The liquid superficial upflow velocity (V-up) and hydraulic retention
time (HRT) on the thermophilic treatment of oleate in expanded granula
r sludge bed (EGSB) reactors were investigated. The highest methane co
nversion rate of oleate, 93 mg CH4-COD/g VSS.d, was attained in a reac
tor operating at a V-up of 1 m/h and an HRT of 24 h. The typical EGSB
reactor hydrodynamics (V-up>4 m/h and HRT<10 h) inhibited the treatmen
t performance, mainly due to biomass washout in particulate form.